CN101829671A - Clean energy utilization method for municipal solid wastes - Google Patents
Clean energy utilization method for municipal solid wastes Download PDFInfo
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- CN101829671A CN101829671A CN 201010160607 CN201010160607A CN101829671A CN 101829671 A CN101829671 A CN 101829671A CN 201010160607 CN201010160607 CN 201010160607 CN 201010160607 A CN201010160607 A CN 201010160607A CN 101829671 A CN101829671 A CN 101829671A
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Abstract
The invention relates to a clean energy utilization method for municipal solid wastes, belonging to the technical field of municipal solid waste treatment and utilization. The process comprises the following steps of: crushing municipal solid wastes and then mixing the municipal solid wastes with coal, wherein the weight ratio of the municipal solid wastes is 20-70 percent; then carrying out heat melting moulding processing to prepare blocks; and carrying out high-temperature pyrolytic carbonization under the airtight, high-temperature and reducing atmosphere by utilizing a coking production facility system, wherein pyrolytic carbonization products are respectively clean high-heat value fuels of solid coke, liquid tar and gas. The invention has the advantages that the municipal solid wastes with complicated components can be treated, complicated municipal waste sorting processes are not needed, the wastes are converted into the high value-added fuels, and meanwhile, the problem of dioxin pollution which is easy to generate in conventional waste energy treatment (the wastes are incinerated to generate electricity) is avoided, thereby having bigger popularization meaning.
Description
Technical field
The invention belongs to urban garbage disposal, utilize technical field, particularly provide a kind of domestic waste clean energy resourceization to utilize method, domestic waste high temperature pyrolysis carbonization treatment.
Technical background
Along with the development in city and the continuous growth of population, the house refuse that produced every day is more and more, Tenth Five-Year Plan Period China's domestic waste amount of clearing will reach 1.58 hundred million tons.Has stacked or 8,000,000,000 tons in all kinds of rubbish of landfill in 600 cities, the whole nation, has 2/3rds city to be surrounded by rubbish.08 is only Beijing's generation house refuse has reached 6,720,000 tons, and is continuous growing trend, and domestic waste has become the outstanding problem of puzzlement capital sustainable development.
At present, the processing method of domestic waste mainly contains sanitary landfills, During High-Temperature Composting, burning, pyrolytic gasification etc. both at home and abroad.
Landfill is the main method that the present most of cities of China solve the house refuse outlet, it is big that sanitary landfills has treating capacity, and operational administrative is fairly simple, and investment and operating cost are low, characteristics such as applicability is strong, but exist recyclable materials in the rubbish and the energy component can not regeneration; Easy polluted underground water of rubbish diffusate and soil, the processing cost height; The foul smell that dumping produces has a strong impact on the problems such as air quality of surrounding enviroment.These shortcomings have restricted the development of landfill.
The compost material mainly is plant class rubbish such as rubbish from cooking and fallen leaves in the domestic waste.The advantage that garbage compost is handled is that cost of investment is little, and is simple to operate, but can not handle the organic matter and the inorganic matter that can not rot, the sorting process complexity, and the expense height, the cycle is long, and sanitary condition is poor; The fertilizer efficiency that produces after the compost treatment is low, cost is high, with chemical fertilizer ratio, sales difficulty, deficiency in economic performance; Many poisonous, harmful substances can enter compost, and the long-term a large amount of compost that use in farmland may cause potentially contaminated.Therefore, garbage compost is handled and is difficult to generally promote in China.
Incineration treatment of garbage is a kind of high-temperature heat treatment technology, and the advantage of burning disposal has: decrement is effective.But waste incineration decrement 80～90% solves the garbage-surrounded city phenomenon effectively; Floor space is little, has saved land resource; Incineration temperature height, rubbish can be utterly destroyed pathogenic substance through high temperature incineration more than 800 ℃ in incinerator, the secondary pollution of having avoided compost and landfill easily to produce.But waste incineration exists investment bigger, the device systems complexity, and the operational administrative difficulty is big, easily produces heavy metal, sour gas He noxious materials such as bioxin, is easy to cause secondary pollution.
Refuse pyrolysis carbonization technology becomes the technological development direction of garbage disposal, its maximum technical advantage just is and can eliminates generation of bioxin extremely toxic substance and diffusion from principle, thereby really realize the clean energy resource processing of rubbish, thoroughly solve the social concern of garbage-surrounded city.High temperature heating domestic waste can effectively be converted into hydrogen chloride with chlorine element in the rubbish under anaerobic condition, has avoided the combination of chlorine element and oxygen element from principle, eliminates the generation of dioxin extremely toxic substance.
Chinese patent (CN17426855A) " city house refuse treatment method and treating apparatus " discloses the device that a kind of rubbish is furnace charge, and furnace chamber inside is in the oxygen deprivation state, by heating municipal refuse is converted into gaseous state, solid product.Patent (CN12777342A) " domestic waste drying, gasifying and melting method of disposal " will be sent into gasification furnace behind the pretreated drying garbage, the gas fuel burning after the gasification, and waste heat is converted into Steam Recovery, and rubbish piece slag is discharged.This type of patented technology belongs to refuse gasification technology category, technology itself does not have and the hydrogen chloride that gasification produces effectively can be separated with other fuel gas, cause the chlorine element directly with other fuel gas directly and the oxygen catalytic combustion, be difficult to avoid the secondary formation of dioxin extremely toxic substance.
Patent (CN1232861A) " with house refuse and or organic waste produce the method and apparatus of hydro carbons " mainly utilize rubbish to produce hydrocarbon by thermal cracking and catalytic pyrolysis, this technology catalytic pyrolysis requires to handle solid residue needs supporting incinerator, and technology is loaded down with trivial details.Simultaneously, this patent need be added catalyst, has increased the operating cost of system.
Patent (CN1644492A) " charcoal production from house refuse " is sent into carbonizing apparatus after with the broken moulding of garbage dewatering and is made semicoke, simultaneously the by-product coke oil and gas.Patent (CN1954044A) " changes into house refuse the Processes and apparatus of carbonaceous fuel " utilizes charing equipment, with the high part destructive distillation of content of organics in the rubbish, destructive distillation product tar is used with the fuel of carbonizing gas as charing equipment.This type of patented technology all exists the calorific value of product pyrolysis (destructive distillation) product coke, tar and coal gas lower, is difficult to realize that further resource and recovery energy are worth, and causes technology to be difficult to generally apply.
At present; existing urban refuse thermal decomposition carbonization technology mainly exists not enough in the following aspects: (1) needs newly-built pyrolysis carbonization device systems and pyrolysis carbonized product secondary operations treatment system; the device systems complexity, initial cost and operating cost are higher, are difficult to accomplish scale production.(2) adopt the independent pyrolysis carbonization treatment of rubbish mostly, pyrolysis carbonized product coke, tar and gas quality are relatively poor, are difficult to realize the economic benefit of technology, have hindered applying of such technology.
Summary of the invention
The object of the present invention is to provide a kind of domestic waste clean energy resourceization to utilize method, overcome the shortcoming and defect part of above-mentioned technology, the present invention utilizes existing ripe coking production technology, under conditions such as high temperature, airtight and reducing atmosphere, domestic waste mixed with coal add object height temperature carbonization treatment, obtain having coke, tar and the coal gas of higher using value, finally reach the target of rubbish processing to be harmless and recycling.
Technology of the present invention is: the broken processing of domestic waste back is mixed with coal, wherein, the shared part by weight of domestic waste is 20%-70%, after handling the system forming blocks through the heat fusing processing and forming again, utilize the coking production device systems, under airtight, high temperature and reducing atmosphere, carry out the high temperature pyrolysis carbonization, the pyrolysis carbonized product is respectively the clean exotic fuels of solid coke, tar liquid, gas.
Domestic waste of the present invention comprise need not sorting process primary house refuse or through organic waste on the sieve after the screening.
Particle size range after the broken processing of described domestic waste is 10mm-50mm.The refuse breaking granularity causes the power consumption of polymer processing height easily less than 10mm, and equipment investment is big; The refuse breaking granularity is brought difficulty to following process easily greater than 50mm.
Described coal is that coal for coking, steam coal or other are used coal.
Described heat fusing processing and forming is handled the system forming blocks, and the heat fusing temperature is controlled to be between 150 ℃-250 ℃, and the density range of machine-shaping piece is 200kg/m
3-800kg/m
3
Type piece after described domestic waste and the coal hybrid process utilizes coking process equipment to carry out high temperature cabonization and handles, and the type piece that domestic waste and coal are made is converted into the 61%-77% coke, 4%-15% tar, 17%-30% coal gas.
Gained coke, tar and coal gas, wherein the calorific value of coke is not less than 12420kJ/Kg, and the calorific value of coal gas is not less than 11301kJ/m
3
Adopt existing ripe coking process system handles rubbish, help reducing the investment and the operating cost of process system, be beneficial to applying of patented technology.Under high temperature, airtight and reducing atmosphere condition,, help on principle, thoroughly eliminating the generation and the diffusion of dioxin extremely toxic substance, realize the harmless treatment of rubbish the high temperature garbage carbonization treatment.Rubbish is mixed common high temperature cabonization with coal, help by the synergy between rubbish and the coal, guarantee the quality of carbonized product coke, tar and coal gas, realize the high added value recovery energy of rubbish, embody social benefit, environmental benefit and the economic benefit of garbage disposal simultaneously.
This technology has following characteristics:
1, can make full use of existing ripe coker system, only need that feed stock for blast furnace is processed in rubbish and coal mixing preliminary treatment and get final product.Process equipment is simple, and investment and operating cost are lower.
2, garbage raw material wide adaptability.Can handle complicated component domestic waste, but comprise crude waste and organic thermal decomposition rubbish, garbage raw material does not need complicated category sorting.
3, system rubbish disposal ability scope is big, efficient height, rubbish that can large, medium and small different scales city.
4, thoroughly avoid the generation and the diffusion of dioxin extremely toxic substance from the technological principle, help realizing the real harmless treatment of rubbish.
5, pyrolysis carbonized product quality is better, can realize high value added utilization, has good economic benefit.
Advantage is, can handle the domestic waste of composition complexity, do not need complicated municipal refuse sorting process, rubbish is changed into high added value fuel, avoid conventional waste energy regeneration to handle in (waste incineration and generating electricity) simultaneously and be easy to generate the pollution problem of De bioxin, had bigger dissemination.
Description of drawings
Fig. 1 utilizes the technical matters flow chart for the domestic waste clean energy resourceization.
The specific embodiment
Implementation process combined process figure of the present invention is described below: domestic waste at first passes through break process, evenly mix according to a certain percentage with coal then, mixed material enters the heat fusing forming processing system, make the rubbish moulded coal, at last, the rubbish moulded coal is joined carry out high temperature cabonization in traditional coking production system and handle.The coke that produces behind the high temperature cabonization, tar and coal gas are as high-quality clean energy resource utilization.
Embodiment 1
Get domestic waste on the 15mm sieve, reclaim magnetisable material by magnetic separation.Be crushed to 20mm, utilize roller drying, detecting dry back msw water content is 8.3%.Coal dust is selected Firing Shenhua Coal for use, and moisture content is 13.4%.According to butt 2kg total amount, the domestic waste adding proportion is 70% to prepare burden, and mixes, and will mixing the material heating, to be compacted to density be 400kg/m
3About, go into 2kg small coke oven experimental provision.100 ℃ of constant temperature is 5 minutes at the stove center, and is persistently overheating then, reaches 960 ℃ of constant temperature at the stove center and closed heating system in 2 minutes.The product productive rate is a coke 68.0%, tar 13.6%, and combustion gas 18.4%, wherein the semicoke calorific value is 12420KJ/Kg, fuel gases calorific value is 13349KJ/m
3
Embodiment 2
Get domestic waste on the 15mm sieve, reclaim magnetisable material by magnetic separation.Be crushed to 20mm, utilize roller drying, detecting dry back msw water content is 8.3%.Coal dust is selected Firing Shenhua Coal for use, and moisture content is 13.4%.According to butt 2kg total amount, the domestic waste adding proportion is 50% to prepare burden, and mixes, and will mixing the material heating, to be compacted to density be 400kg/m
3About, go into 2kg small coke oven experimental provision.100 ℃ of constant temperature is 5 minutes at the stove center, and is persistently overheating then, reaches 960 ℃ of constant temperature at the stove center and closed heating system in 2 minutes.The product productive rate is a coke 70.0%, tar 10.2%, and combustion gas 19.8%, wherein the semicoke calorific value is 16240KJ/Kg, fuel gases calorific value is 11698KJ/m
3
Embodiment 3
Get domestic waste on the 15mm sieve, reclaim magnetisable material by magnetic separation.Be crushed to 20mm, utilize roller drying, detecting dry back msw water content is 8.3%.Coal dust is selected Firing Shenhua Coal for use, and moisture content is 13.4%.According to butt 2kg total amount, the domestic waste adding proportion is 30% to prepare burden, and mixes, and will mixing the material heating, to be compacted to density be 400kg/m
3About, go into 2kg small coke oven experimental provision.100 ℃ of constant temperature is 5 minutes at the stove center, and is persistently overheating then, reaches 960 ℃ of constant temperature at the stove center and closed heating system in 2 minutes.The product productive rate is a coke 68.8%, tar 4.4%, and combustion gas 26.8%, wherein the semicoke calorific value is 22720KJ/Kg, fuel gases calorific value is 13231KJ/m
3
Claims (7)
1. a domestic waste clean energy resourceization is utilized method, it is characterized in that: the broken processing of domestic waste back is mixed with coal, wherein, the shared part by weight of domestic waste is 20%-70%, after handling the system forming blocks through the heat fusing processing and forming again, utilize the coking production device systems, under airtight, high temperature and reducing atmosphere, carry out the high temperature pyrolysis carbonization, the pyrolysis carbonized product is respectively the clean exotic fuels of solid coke, tar liquid, gas.
2. method according to claim 1 is characterized in that, described domestic waste comprise need not sorting process primary house refuse or through organic waste on the sieve after the screening.
3. according to claim 1 described method, it is characterized in that the particle size range after the broken processing of described domestic waste is 10mm-50mm.The refuse breaking granularity causes the power consumption of polymer processing height easily less than 10mm, and equipment investment is big; The refuse breaking granularity is brought difficulty to following process easily greater than 50mm.
4. method according to claim 1 is characterized in that, described coal is that coal for coking, steam coal or other are used coal.
5. method according to claim 1 is characterized in that, described heat fusing processing and forming is handled the system forming blocks, and the heat fusing temperature is controlled to be between 150 ℃-250 ℃, and the density range of machine-shaping piece is 200kg/m
3-800kg/m
3
6. method according to claim 1, it is characterized in that, type piece after described domestic waste and the coal hybrid process utilizes coking process equipment to carry out high temperature cabonization and handles, the type piece that domestic waste and coal are made is converted into the 61%-77% coke, 4%-15% tar, 17%-30% coal gas.
7. method according to claim 6 is characterized in that, gained coke, tar and coal gas, and wherein the calorific value of coke is not less than 12420kJ/Kg, and the calorific value of coal gas is not less than 11301kJ/m
3
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010160607 CN101829671A (en) | 2010-04-26 | 2010-04-26 | Clean energy utilization method for municipal solid wastes |
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| CN 201010160607 CN101829671A (en) | 2010-04-26 | 2010-04-26 | Clean energy utilization method for municipal solid wastes |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103842103A (en) * | 2011-08-25 | 2014-06-04 | 索伦环境和设备电气有限公司 | Method for treating solid waste based on a gradient composed of two different heat sources |
| CN104646391A (en) * | 2014-12-18 | 2015-05-27 | 无锡荣博能源环保科技有限公司 | Kitchen waste energy treatment process |
| CN106929079A (en) * | 2015-12-30 | 2017-07-07 | 北京三聚环保新材料股份有限公司 | It is a kind of to be suitable to the molding mass containing low-order coal and rubbish of tamping coking |
| CN107236559A (en) * | 2016-03-29 | 2017-10-10 | 北京三聚环保新材料股份有限公司 | A kind of handling process of rubbish |
| CN111748394A (en) * | 2020-06-04 | 2020-10-09 | 北京科技大学 | Method and system for pre-treating and upgrading urban solid waste by granulation |
| CN112077125A (en) * | 2020-09-15 | 2020-12-15 | 四川同益环境科技有限责任公司 | Energy treatment method for household garbage |
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| JPH039989A (en) * | 1989-06-06 | 1991-01-17 | Nkk Corp | Production of coke |
| DE19538921C2 (en) * | 1995-10-19 | 2000-03-09 | Int Vermittlungsgesellschaft F | Process for processing organic waste materials, in particular plastics |
| CN1465655A (en) * | 2002-07-04 | 2004-01-07 | 首钢总公司 | High temp. dry distillation treatment method for urban domestic refuse |
| CN1465656A (en) * | 2002-07-04 | 2004-01-07 | 首钢总公司 | Waste plastics and coal cocoaking treatment method |
| CN1502848A (en) * | 2002-11-20 | 2004-06-09 | 首钢总公司 | Method and system for treating hospital refuse by utilizing coking technology |
| CN1555932A (en) * | 2004-01-01 | 2004-12-22 | 侯祥峰 | Garbage treatment technique |
| CN1580189A (en) * | 2003-08-01 | 2005-02-16 | 首钢总公司 | Waste plastic processing method for increasing coke strength and its apparatus system |
| CN1644492A (en) * | 2004-12-10 | 2005-07-27 | 彭立军 | Charcoal production from house refuse |
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2010
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Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH039989A (en) * | 1989-06-06 | 1991-01-17 | Nkk Corp | Production of coke |
| DE19538921C2 (en) * | 1995-10-19 | 2000-03-09 | Int Vermittlungsgesellschaft F | Process for processing organic waste materials, in particular plastics |
| CN1465655A (en) * | 2002-07-04 | 2004-01-07 | 首钢总公司 | High temp. dry distillation treatment method for urban domestic refuse |
| CN1465656A (en) * | 2002-07-04 | 2004-01-07 | 首钢总公司 | Waste plastics and coal cocoaking treatment method |
| CN1502848A (en) * | 2002-11-20 | 2004-06-09 | 首钢总公司 | Method and system for treating hospital refuse by utilizing coking technology |
| CN1580189A (en) * | 2003-08-01 | 2005-02-16 | 首钢总公司 | Waste plastic processing method for increasing coke strength and its apparatus system |
| CN1555932A (en) * | 2004-01-01 | 2004-12-22 | 侯祥峰 | Garbage treatment technique |
| CN1644492A (en) * | 2004-12-10 | 2005-07-27 | 彭立军 | Charcoal production from house refuse |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103842103A (en) * | 2011-08-25 | 2014-06-04 | 索伦环境和设备电气有限公司 | Method for treating solid waste based on a gradient composed of two different heat sources |
| CN103842103B (en) * | 2011-08-25 | 2016-04-13 | 索伦环境和设备电气有限公司 | Based on the solid waste substance treating method of the gradient be made up of two different heat sources |
| CN104646391A (en) * | 2014-12-18 | 2015-05-27 | 无锡荣博能源环保科技有限公司 | Kitchen waste energy treatment process |
| CN106929079A (en) * | 2015-12-30 | 2017-07-07 | 北京三聚环保新材料股份有限公司 | It is a kind of to be suitable to the molding mass containing low-order coal and rubbish of tamping coking |
| CN107236559A (en) * | 2016-03-29 | 2017-10-10 | 北京三聚环保新材料股份有限公司 | A kind of handling process of rubbish |
| CN111748394A (en) * | 2020-06-04 | 2020-10-09 | 北京科技大学 | Method and system for pre-treating and upgrading urban solid waste by granulation |
| CN112077125A (en) * | 2020-09-15 | 2020-12-15 | 四川同益环境科技有限责任公司 | Energy treatment method for household garbage |
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Open date: 20100915 |